Rare earth aluminates and gallates supported rhodium catalysts for catalytic partial oxidation of hydrocarbons
a technology of rhodium catalyst and rare earth aluminates, which is applied in the direction of metal/metal-oxide/metal-hydroxide catalyst, combustible gas purification/modification, chemical production, etc., can solve the problems of catalyst deactivation, reaction that is simply too slow and/or efficient to be economical, and uneconomical at best and ineffective at worst, so as to improve the composition of the catalys
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example 1
[0034]A rare earth (La) modified support material was prepared using a standard incipient wetness technique. 20 g of alpha alumina (30–50 mesh) was impregnated with an aqueous solution of La(NO3)3. The impregnated material was then dried in an oven at 100° C. overnight. The support material was further calcined at 1050° C. in air for 2 hours to allow the solid-state reaction between the alumina and lanthanum nitrate to take place. After calcination, the composition was found to be 6.40 wt % LaAlO3 on Al2O3.
example 2
[0035]A rare earth (Sm) modified support material was prepared using a standard incipient wetness technique. 20 g of alpha alumina (30–50 mesh) impregnated with an aqueous solution of Sm(NO3)3. The impregnated material was then dried in an oven at 100° C. overnight. The support material was further calcined at 1050° C. in air for 2 hours to allow the solid-state reaction between the alumina and samarium nitrate to take place. After calcination, the composition was found to be 6.79 wt % SmAlO3 on Al2O3.
example 3
[0036]Catalyst A was prepared from the rare earth modified support material in Example 1. The catalyst was prepared by incipient wetness impregnation of the LaAlO3 / Al2O3 particulate support material with a aqueous solution of rhodium chloride hydrate (RhCl3.xH2O. The nominal loading for Rh was 4% by weight. The rhodium impregnated modified support was dried at 100° C. overnight and then calcined at 600° C. in air for 3 hours. The calcined catalyst precursor was then reduced in a tube furnace under a flow of 300 ml / 300 ml H2 / N2 at 500° C. for 3 hours prior to catalytic testing.
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